EP0322290A2 - Process for the allylation of perhaloalkyl, perhaloalkoxy, perhaloalkylthio anilines in the presence of metals - Google Patents

Process for the allylation of perhaloalkyl, perhaloalkoxy, perhaloalkylthio anilines in the presence of metals Download PDF

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EP0322290A2
EP0322290A2 EP88403213A EP88403213A EP0322290A2 EP 0322290 A2 EP0322290 A2 EP 0322290A2 EP 88403213 A EP88403213 A EP 88403213A EP 88403213 A EP88403213 A EP 88403213A EP 0322290 A2 EP0322290 A2 EP 0322290A2
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process according
palladium
chosen
allyl
chloride
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EP0322290A3 (en
EP0322290B1 (en
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Jean-Roger Desmurs
Jean-Pierre Lecouve
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Rhodia Chimie SAS
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Rhone Poulenc Chimie SA
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/04Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups
    • C07C209/06Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups by substitution of halogen atoms
    • C07C209/10Preparation of compounds containing amino groups bound to a carbon skeleton by substitution of functional groups by amino groups by substitution of halogen atoms with formation of amino groups bound to carbon atoms of six-membered aromatic rings or from amines having nitrogen atoms bound to carbon atoms of six-membered aromatic rings

Definitions

  • the present invention relates to a process for the preparation of N-allyl perhaloalkyl, perhaloalkoxy, perhaloalkylthio anilines. It relates more particularly to a process for allylation of metatrifluoromethylaniline in the presence of metals.
  • allylation yield is around 50%. This yield is of paramount importance when the raw materials are very expensive. Thus, in the case of metatrifluoromethylaniline, it is sought to obtain yields as high as possible. In the case of aminophenols this criterion is much less important.
  • metatrifluoromethylaniline is a compound which is highly deactivated from the chemical point of view, the substitution of which is much more difficult than that of derivatives such as paraphenylenediamine, which is activated and therefore promotes substitutions.
  • the present invention has achieved this dual objective. Its subject is a process for allylating perhaloalkyl, perhaloalkoxy, perhaloalkylthioanilines, characterized in that an aniline is brought into contact in a solvent medium. perhaloalkylated, perhaloalkoxylated or perhalogenothioalkylated with an allyl halide in the presence of a catalytic amount of a metal chosen from palladium, copper and nickel.
  • perhaloalkylated, perhaloalkoxylated or perhalogenothioalkylated aniline is understood to mean the compounds of general formula (I) below: in which : - A represents a covalent bond, an oxygen or sulfur atom, - X1, X2, X3, X4, X5 each represents an identical or different halogen atom, - n is equal to 0.1 or 2, - R represents a hydrogen atom, a halogen, an alkyl group having 1 to 4 carbon atoms, alkoxy having 1 to 4 carbon atoms, aryl.
  • the process of the present invention is catalyzed as indicated above by a metal chosen from palladium, copper and nickel.
  • metals can be in the form of metal salts in the oxidation state I or II, in particular chloride, sulfate, acetate, oxide.
  • these salts, oxides and complexes there may be mentioned - palladium chloride, - cuprous chloride, - cupric chloride, - nickel chloride, - palladium sulfate, - copper sulphate - nickel sulfate, - cupric oxide, - palladium acetate, - cupric acetate, - Palladium chloride complexed with benzonitrile.
  • the metal can also be in the oxidation state O in metallic form such as copper powder for example or in the form of a complex such as palladium dibenzylideneacetone. Among the metals mentioned, it is preferred to use palladium.
  • the allyl halide is preferably chosen from allyl chloride and allyl bromide, it is still preferred to use allyl chloride.
  • the present invention can be implemented in polar aprotic solvents such as: - N-methylpyrrolidone (NMP), - N, N-dimethylformamide (DMF), - N-methylformamide (NMF), - N, N-dimethylacetamide (DMA), in ethers such as: - tetrahydrofuran (THF), - petroleum ether, - methyltertiobutylether, in nitriles such as: - benzonitrile, - acetonitrile, in optionally halogenated aromatic solvents such as: - toluene, - xylene, - chlorobenzene, - dichlorobenzene, in aliphatic solvents preferably containing 5 to 10 optionally halogenated carbon atoms such as: - cyclohexane, - heptane, in alcohols and preferably in ethanol.
  • NMP N-methylpyrrolidone
  • polar aprotic solvents it is preferred to use polar aprotic solvents.
  • a molar ratio of allyl halide to aniline of between 1 and 2 and a molar ratio of the metal catalyst to aniline of between 0.01 and 0 , 5 preferably between 0.05 and 0.2.
  • the concentration of aniline in the solvent is preferably between 100 g and 500 g per liter.
  • reaction conditions it is preferred to work between 50 and 120 ° C. for a period which can vary between 2 and 24 hours.
  • the mixture is stirred and heated to 75 ° for variable times. After cooling, 5 ml of sodium hydroxide are added. The organic products are extracted with 5 ⁇ 5 ml of isopropyl ether. The organic phase is filtered through clarcel and diluted to 25 ml to be determined by internal calibration by gas phase chromatography.
  • Example 1 Solvent influence Test Catalyst Solvent Time TT m-TFMA RT N-Allyl RT N, N-Diallyl Comparison 5 - 0 ⁇ -0-0 ⁇ 2:30 a.m. 0.3 Traces - 19 Cu 0 ⁇ -0-0 ⁇ 2:30 a.m. 18.4 77 16 Comparison 6 - DMF 2:30 a.m. 17.8 76.8 - 20 Cu DMF 2:30 a.m. 67.6 62.9 16.7 Comparison 7 - Toluene 2:30 a.m. 1.1 Traces - 21 Cu Toluene 2:30 a.m.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A new process for allylation of perhaloalkyl, perhaloalkoxy and perhaloalkylthio anilines with an allyl halide in the presence of metals such as copper and palladium. <??>The invention enables the allylation yields to be markedly increased.

Description

La présente invention concerne un procédé de préparation de N-allyl perhalogénoalkyl, perhalogénoalcoxy, perhalogénoalkylthio anilines. Elle concerne plus particulièrement un procédé d'allylation de la métatrifluorométhylaniline en présence de métaux.The present invention relates to a process for the preparation of N-allyl perhaloalkyl, perhaloalkoxy, perhaloalkylthio anilines. It relates more particularly to a process for allylation of metatrifluoromethylaniline in the presence of metals.

Il est connu par exemple selon le brevet US 2 286 678 de condenser le bromure d'allyle sur un aminophénol en présence de carbonate de potassium dans un solvant alcoolique.It is known, for example, according to US Pat. No. 2,286,678 to condense allyl bromide on an aminophenol in the presence of potassium carbonate in an alcoholic solvent.

Le rendement d'allylation se situe aux environs de 50 %. Ce rendement présente une importance capitale lorsque les matières premières sont très couteuses. Ainsi dans le cas de la métatrifluorométhylaniline on cherche à obtenir des rendements aussi élévés que possible. Dans le cas des aminophénols ce critère est beaucoup moins important.The allylation yield is around 50%. This yield is of paramount importance when the raw materials are very expensive. Thus, in the case of metatrifluoromethylaniline, it is sought to obtain yields as high as possible. In the case of aminophenols this criterion is much less important.

Il est aussi connu d'après le brevet US 3 668 254 de préparer les N-haloallyl p. phénylène diamines par condensation sur l'amino-4 diphénylamine de dichloro-2,3 propène en présence de quantités stoechiométriques de triéthylamine et en l'absence de solvant.It is also known from US Pat. No. 3,668,254 to prepare N-haloallyl p. phenylene diamines by condensation on the amino 4-diphenylamine of 2,3-dichloro propene in the presence of stoichiometric amounts of triethylamine and in the absence of solvent.

Les rendements annoncés dans ledit brevet sont toujours très faibles, environ 38 % dans le seul exemple. La technique décrite dans ce brevet n'était donc pas transposable à des matières premières aussi onéreuses que la métatrifluorométhylaniline.The yields announced in said patent are still very low, around 38% in the single example. The technique described in this patent was therefore not transposable to raw materials as expensive as metatrifluoromethylaniline.

Il faut aussi noter que la métatrifluorométhylaniline est un composé fortement désactivé du point de vue chimique dont la substitution est beaucoup plus difficile que celle des dérivés tels que la paraphénylènediamine qui elle est activée et favorise donc les substitutions.It should also be noted that metatrifluoromethylaniline is a compound which is highly deactivated from the chemical point of view, the substitution of which is much more difficult than that of derivatives such as paraphenylenediamine, which is activated and therefore promotes substitutions.

L'industrie se trouve devant un double problème, obtenir une N-allylation de la métatrifluorométhylaniline avec des rendements corrects sur un produit qui est beaucoup plus difficile à substituer que ceux qui sont décrits dans l'art antérieur.The industry is faced with a double problem, obtaining an N-allylation of metatrifluoromethylaniline with correct yields on a product which is much more difficult to replace than those which are described in the prior art.

La présente invention a permis d'atteindre ce double objectif. Elle a pour objet un procédé d'allylation des perhalogénoalkyl, perhalogénoalcoxy, perhalogénoalkylthioanilines caractérisé en ce que on met en contact en milieu solvant une aniline perhalogénoalkylée, perhalogénoalcoxylée ou perhalogénothioalkylée avec un halogénure d'allyle en présence d'une quantité catalytique d'un métal choisi parmi le palladium, le cuivre et le nickel.The present invention has achieved this dual objective. Its subject is a process for allylating perhaloalkyl, perhaloalkoxy, perhaloalkylthioanilines, characterized in that an aniline is brought into contact in a solvent medium. perhaloalkylated, perhaloalkoxylated or perhalogenothioalkylated with an allyl halide in the presence of a catalytic amount of a metal chosen from palladium, copper and nickel.

On entend par aniline perhalogénoalkylée, perhalogénoalcoxylée ou perhalogénothioalkylée les composés de formule générale (I) suivante :

Figure imgb0001
dans laquelle :
- A représente une liaison covalente, un atome d'oxygène ou de soufre,
- X₁, X₂, X₃, X₄, X₅ représente chacun un atome d'halogène identique ou différent,
- n est égal à 0,1 ou 2,
- R représente un atome d'hydrogène, un halogène, un groupe alkyle ayant 1 à 4 atomes de carbone, alcoxy ayant 1 à 4 atomes de carbone, aryle.The term perhaloalkylated, perhaloalkoxylated or perhalogenothioalkylated aniline is understood to mean the compounds of general formula (I) below:
Figure imgb0001
in which :
- A represents a covalent bond, an oxygen or sulfur atom,
- X₁, X₂, X₃, X₄, X₅ each represents an identical or different halogen atom,
- n is equal to 0.1 or 2,
- R represents a hydrogen atom, a halogen, an alkyl group having 1 to 4 carbon atoms, alkoxy having 1 to 4 carbon atoms, aryl.

Ces anilines sont toutes des composés fortement désactivés dont la substitution est difficile.These anilines are all highly deactivated compounds whose substitution is difficult.

Il est encore connu d'après le brevet US 3 642 902 de réaliser l'allylation de l'aniline, composé non désactivé, par des complexes du chlorure de bis(allylpalladium). Les rendements d'allylation sont toujours faibles, ils sont de l'ordre de 25 %.It is also known from US Pat. No. 3,642,902 to carry out the allylation of the aniline, a compound which is not deactivated, with complexes of bis (allyl palladium) chloride. The allylation yields are always low, they are around 25%.

Il est aussi connu d'après les articles de ARESTA parus dans Synth. React. Inorg. Met. Org. Chem., 9(2), 157-174 de 1979 et dans le Journal of Chemical Society Dalton, (1977), 493 de préparer des complexes du palladium II avec les N-allylanilines. Ces complexes sont facilement détruits avec libération de méthylacétylène et d'un complexe Pd-aniline. A la lecture de ces trois derniers documents, il était impossible d'envisager un procédé industriel mettant en oeuvre des métaux tels que le palladium du fait des risques de formation de ces complexes qui conduisent à une rétrogradation irréversible des N-allylanilines formées à la moindre augmentation de température.It is also known from the articles of ARESTA published in Synth. React. Inorg. Met. Org. Chem., 9 (2), 157-174 of 1979 and in the Journal of Chemical Society Dalton, (1977), 493 to prepare complexes of palladium II with N-allylanilines. These complexes are easily destroyed with the release of methylacetylene and a Pd-aniline complex. On reading these last three documents, it was impossible to envisage an industrial process using metals such as palladium because of the risks of formation of these complexes which lead to an irreversible retrogradation of the N-allylanilines formed at the slightest increase in temperature.

Aussi il a été tout à fait surprenant de constater qu'en mettant en contact une aniline perhalogénoalkylée, perhalogénoalcoxylée ou perhalogénothioalkylée avec un métal choisi parmi le palladium, le nickel et le cuivre il n'y ait aucune dégradation de la N-allylaniline formée et un excellent rendement calculé sur l'aniline transformée.Also, it was quite surprising to find that by contacting a perhaloalkylated, perhaloalkoxylated or perhalogenothioalkylated aniline with a metal chosen from palladium, nickel and copper there is no degradation of the N-allylaniline formed and an excellent yield calculated on the processed aniline.

Le procédé de la présente invention est catalysé comme indiqué précédemment par un métal choisi parmi le palladium, le cuivre et le nickel. Ces métaux peuvent se présenter sous forme de sels métalliques à l'état d'oxydation I ou II notamment de chlorure, de sulfate, d'acétate, d'oxyde. Parmi ces sels, oxydes et complexes on peut citer
- le chlorure de palladium,
- le chlorure cuivreux,
- le chlorure cuivrique,
- le chlorure de nickel,
- le sulfate de palladium,
- le sulfate de cuivre
- le sulfate de nickel,
- l'oxyde cuivrique,
- l'acétate de palladium,
- l'acétate cuivrique,
- le chlorure de palladium complexé par le benzonitrile.
The process of the present invention is catalyzed as indicated above by a metal chosen from palladium, copper and nickel. These metals can be in the form of metal salts in the oxidation state I or II, in particular chloride, sulfate, acetate, oxide. Among these salts, oxides and complexes there may be mentioned
- palladium chloride,
- cuprous chloride,
- cupric chloride,
- nickel chloride,
- palladium sulfate,
- copper sulphate
- nickel sulfate,
- cupric oxide,
- palladium acetate,
- cupric acetate,
- Palladium chloride complexed with benzonitrile.

Le métal peut aussi se présenter à l'état d'oxydation O sous forme métallique telle que la poudre de cuivre par exemple ou sous forme de complexe tel que le palladium dibenzylidèneacétone. On préfère parmi les métaux cités utiliser le palladium.The metal can also be in the oxidation state O in metallic form such as copper powder for example or in the form of a complex such as palladium dibenzylideneacetone. Among the metals mentioned, it is preferred to use palladium.

L'halogénure d'allyle est choisi de préférence parmi le chlorure d'allyle et le bromure d'allyle, on préfère encore utiliser le chlorure d'allyle.The allyl halide is preferably chosen from allyl chloride and allyl bromide, it is still preferred to use allyl chloride.

La présente invention peut être mise en oeuvre dans les solvants aprotiques polaires tels que :
- la N-méthylpyrrolidone (NMP),
- le N,N-diméthylformamide (DMF),
- le N-méthylformamide (NMF),
- le N,N-diméthylacétamide (DMA),
dans des éthers tels que :
- le tetrahydrofurane (THF),
- l'éther de pétrole,
- le méthyltertiobutyléther,
dans des nitriles tels que :
- le benzonitrile,
- l'acétonitrile,
dans des solvants aromatiques éventuellement halogénés tels que :
- le toluène,
- le xylène,
- le chlorobenzène,
- le dichlorobenzène,
dans des solvants aliphatiques contenant de préférence 5 à 10 atomes de carbone éventuellement halogénés tels que :
- le cyclohexane,
- l'heptane,
dans des alcools et de préférence dans l'éthanol.
The present invention can be implemented in polar aprotic solvents such as:
- N-methylpyrrolidone (NMP),
- N, N-dimethylformamide (DMF),
- N-methylformamide (NMF),
- N, N-dimethylacetamide (DMA),
in ethers such as:
- tetrahydrofuran (THF),
- petroleum ether,
- methyltertiobutylether,
in nitriles such as:
- benzonitrile,
- acetonitrile,
in optionally halogenated aromatic solvents such as:
- toluene,
- xylene,
- chlorobenzene,
- dichlorobenzene,
in aliphatic solvents preferably containing 5 to 10 optionally halogenated carbon atoms such as:
- cyclohexane,
- heptane,
in alcohols and preferably in ethanol.

Parmi ces solvants on préfère utiliser les solvants aprotiques polaires.Among these solvents, it is preferred to use polar aprotic solvents.

En ce qui concerne les quantités de réactifs mises en oeuvre on préfère utiliser un rapport molaire d'halogénure d'allyle à l'aniline compris entre 1 et 2 et un rapport molaire du catalyseur métallique à l'aniline comprise entre 0,01 et 0,5 de préférence compris entre 0,05 et 0,2.As regards the amounts of reagents used, it is preferred to use a molar ratio of allyl halide to aniline of between 1 and 2 and a molar ratio of the metal catalyst to aniline of between 0.01 and 0 , 5 preferably between 0.05 and 0.2.

La concentration de l'aniline dans le solvant est comprise de préférence entre 100 g et 500 g par litre.The concentration of aniline in the solvent is preferably between 100 g and 500 g per liter.

En ce qui concerne les conditions réactionnelles on préfère travailler entre 50 et 120°C pendant une période pouvant évoluer entre 2 et 24 heures.As regards the reaction conditions, it is preferred to work between 50 and 120 ° C. for a period which can vary between 2 and 24 hours.

La présente invention sera plus complètement décrite à l'aide des exemples suivants qui ne doivent en aucun cas être considérés comme limitatifs.The present invention will be more fully described with the aid of the following examples which are in no way to be considered as limiting.

Dans les exemples suivants on entend par :
TT = le taux de transformation du produit initial

Figure imgb0002
RT = le rendement sur produit transformé
Figure imgb0003
In the following examples:
TT = the transformation rate of the initial product
Figure imgb0002
RT = yield on processed product
Figure imgb0003

EXEMPLES 1 à 16EXAMPLES 1 to 16

Dans un réacteur de 30 ml, on introduit
- 0.65 g de m. trifluorométhylaniline (4 m Moles),
- 0,61 g de chlorure d'alkyle (8 m Moles),
- 2 ml de solvant,
- 0,4 mM de catalyseur.
The following are introduced into a 30 ml reactor
- 0.65 g of m. trifluoromethylaniline (4 m Moles),
- 0.61 g of alkyl chloride (8 m Moles),
- 2 ml of solvent,
- 0.4 mM of catalyst.

Le mélange est agité et chauffé à 75° pendant des temps variables. Après refroidissement, on ajoute 5 ml de soude N. Les produits organiques sont extraits par 5 x 5 ml d'éther isopropylique. La phase organique est filtrée sur clarcel et diluée à 25 ml pour être dosée par étalonnage interne en chromatographie phase gazeuse.

Figure imgb0004
Figure imgb0005
The mixture is stirred and heated to 75 ° for variable times. After cooling, 5 ml of sodium hydroxide are added. The organic products are extracted with 5 × 5 ml of isopropyl ether. The organic phase is filtered through clarcel and diluted to 25 ml to be determined by internal calibration by gas phase chromatography.
Figure imgb0004
Figure imgb0005

EXEMPLES 17 à 18EXAMPLES 17 to 18

Dans réacteur de 30 ml, on introduit
- 0,65 g de m. trifluorométhylaniline (4m Moles),
- 0,3 g de chlorure d'allyle (4 m Moles),
- 2 ml de solvant,
- 0,4 mM de catalyseur.
Into a 30 ml reactor, the following are introduced
- 0.65 g of m. trifluoromethylaniline (4m Moles),
- 0.3 g of allyl chloride (4 moles),
- 2 ml of solvent,
- 0.4 mM of catalyst.

Le mélange est chauffé et agité 2 H 30 à 75°. Après refroidissement, on ajoute 5 ml de soude N. Les produits organiques sont extraits par 5 x 5 ml d'éther isopropylique. La phase organique est filtrée sur clarcel et diluée à 25 ml pour être dosée par étalonnage interne. Essai Catalyseur Solvant Temps TT m-TFMA RT N-Allyl RT N,N-Diallyl Invention 17 Pd(OAc)₂ Heptane 2 H 30 23,7 5,7 Invention 18 Cu₂O Heptane 2 H 30 39,3 54,1 11 % The mixture is heated and stirred for 2 h 30 min at 75 °. After cooling, 5 ml of sodium hydroxide are added. The organic products are extracted with 5 × 5 ml of isopropyl ether. The organic phase is filtered through clarcel and diluted to 25 ml to be determined by internal calibration. Test Catalyst Solvent Time TT m-TFMA RT N-Allyl RT N, N-Diallyl Invention 17 Pd (OAc) ₂ Heptane 2:30 a.m. 23.7 5.7 Invention 18 Cu₂O Heptane 2:30 a.m. 39.3 54.1 11%

EXEMPLES 19 à 23EXAMPLES 19 to 23

Dans ces exemples a été étudié l'influence de différents solvants dans les conditions de l'exemple 1. Influence du solvant Essai Catalyseur Solvant Temps TT m-TFMA RT N-Allyl RT N,N-Diallyl Comparatif 5 - 0̸-0-0̸ 2 H 30 0,3 Traces - 19 Cu 0̸-0-0̸ 2 H 30 18,4 77 16 Comparatif 6 - DMF 2 H 30 17,8 76,8 - 20 Cu DMF 2 H 30 67,6 62,9 16,7 Comparatif 7 - Toluène 2 H 30 1,1 Traces - 21 Cu Toluène 2 H 30 21,2 69,9 5,9 Comparatif 8 - NMP 2 H 30 16,9 85 - 22 Cu NMP 2 H 30 80,4 66,7 3 Comparatif 9 - DMF - H₂O 2ml - 1ml 2 H 30 74 42 9,4 23 Cu DMF - H₂O 2ml - 1ml 2 H 30 95,6 15,9 44,5 In these examples, the influence of different solvents was studied under the conditions of Example 1. Solvent influence Test Catalyst Solvent Time TT m-TFMA RT N-Allyl RT N, N-Diallyl Comparison 5 - 0̸-0-0̸ 2:30 a.m. 0.3 Traces - 19 Cu 0̸-0-0̸ 2:30 a.m. 18.4 77 16 Comparison 6 - DMF 2:30 a.m. 17.8 76.8 - 20 Cu DMF 2:30 a.m. 67.6 62.9 16.7 Comparison 7 - Toluene 2:30 a.m. 1.1 Traces - 21 Cu Toluene 2:30 a.m. 21.2 69.9 5.9 Comparison 8 - NMP 2:30 a.m. 16.9 85 - 22 Cu NMP 2:30 a.m. 80.4 66.7 3 Comparative 9 - DMF - H₂O 2ml - 1ml 2:30 a.m. 74 42 9.4 23 Cu DMF - H₂O 2ml - 1ml 2:30 a.m. 95.6 15.9 44.5

Claims (10)

1 - Procédé de préparation de N-allylperhalogénoalkyl, - perhalogénoalcoxy, perhalogénoalkylthio anilines caractérisé en ce que on met en contact une aniline perhalogénoalkylée, - perhalogénoalcoxylée, perhalogénothioalkylée en milieu solvant avec un halogénure d'allyle en présence d'une quantité catalytique d'un métal choisi parmi le palladium, le cuivre et le nickel.1 - Process for the preparation of N-allylperhaloalkyl, - perhaloalkoxy, perhaloalkylthio anilines characterized in that a perhaloalkylated aniline is brought into contact, - perhaloalkoxylated, perhalogenothioalkylated in a solvent medium with an allyl halide in the presence of a catalytic amount metal chosen from palladium, copper and nickel. 2 - Procédé selon la revendication 1 caractérisé en ce que l'aniline répond à la formule générale (I) suivante :
Figure imgb0006
dans laquelle
- A représente une liaison covalente, un atome d'oxygène ou de soufre,
- X₁,X₂,X₃,X₄,X₅ représente chacun un atome d'halogène identique ou différent.
- n est égal à 0,1 ou 2,
- R représente un atome d'hydrogène, un halogène, un groupe alkyle ayant 1 à 4 atomes de carbone, alcoxy ayant 1 à 4 atomes de carbone, aryle.
2 - Process according to claim 1 characterized in that the aniline corresponds to the following general formula (I):
Figure imgb0006
in which
- A represents a covalent bond, an oxygen or sulfur atom,
- X₁, X₂, X₃, X₄, X₅ each represents an identical or different halogen atom.
- n is equal to 0.1 or 2,
- R represents a hydrogen atom, a halogen, an alkyl group having 1 to 4 carbon atoms, alkoxy having 1 to 4 carbon atoms, aryl.
3 - Procédé selon la revendication 2 caractérisé en ce que le composé de formule (I) est représenté par la trifluorométhylaniline.3 - Process according to claim 2 characterized in that the compound of formula (I) is represented by trifluoromethylaniline. 4 - Procédé selon la revendication 1 caractérisé en ce que l'halogénure d'allyle est choisi parmi le chlorure et le bromure d'allyle et est de préférence le chlorure d'allyle.4 - Process according to claim 1 characterized in that the allyl halide is chosen from chloride and allyl bromide and is preferably allyl chloride. 5 - Procédé selon la revendication 1 caractérisé en ce que le métal est le palladium.5 - Process according to claim 1 characterized in that the metal is palladium. 6 - Procédé selon les revendications 1 et 5 caractérisé en ce que le catalyseur est choisi parmi le diacétate de palladium et le palladium dibenzylidène acétone.6 - Process according to claims 1 and 5 characterized in that the catalyst is chosen from palladium diacetate and palladium dibenzylidene acetone. 7 - Procédé selon la revendication 1 caractérisé en ce que le solvant est choisi parmi l'heptane et l'acétonitrile.7 - Process according to claim 1 characterized in that the solvent is chosen from heptane and acetonitrile. 8 - Procédé selon la revendication 1 caractérisé en ce que le rapport molaire de l'halogénure d'alkyle à la métatrifluorométhylaniline est compris entre 1 et 2.8 - Process according to claim 1 characterized in that the molar ratio of alkyl halide to metatrifluoromethylaniline is between 1 and 2. 9 - Procédé selon la revendication 1 caractérisé en ce que la température réactionnelle est comprise entre 50 et 120°C.9 - Process according to claim 1 characterized in that the reaction temperature is between 50 and 120 ° C. 10 - Procédé selon la revendication 1 caractérisé en ce que le rapport molaire du catalyseur métallique à la N-métatrifluorométhylaniline est compris entre 0,01 et 0,5 et de préférence entre 0,05 et 0,2.10 - Process according to claim 1 characterized in that the molar ratio of the metal catalyst to N-metatrifluoromethylaniline is between 0.01 and 0.5 and preferably between 0.05 and 0.2.
EP88403213A 1987-12-23 1988-12-16 Process for the allylation of perhaloalkyl, perhaloalkoxy, perhaloalkylthio anilines in the presence of metals Expired - Lifetime EP0322290B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT88403213T ATE89259T1 (en) 1987-12-23 1988-12-16 PROCESS FOR THE ALLYLATION OF PERHALOALKYL, PERHALOALKOXY, PERHALOALKYLTHIOANILINES IN THE PRESENCE OF METALS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8718011A FR2625196B1 (en) 1987-12-23 1987-12-23 PROCESS FOR ALLYLATION OF PERHALOGENOALKYL, PERHALOGENOALCOXY, PERHALOGENOALKYLTHIO ANILINES IN THE PRESENCE OF METALS
FR8718011 1987-12-23

Publications (3)

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EP0322290A2 true EP0322290A2 (en) 1989-06-28
EP0322290A3 EP0322290A3 (en) 1990-05-02
EP0322290B1 EP0322290B1 (en) 1993-05-12

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US (1) US4956496A (en)
EP (1) EP0322290B1 (en)
JP (1) JPH02739A (en)
AT (1) ATE89259T1 (en)
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FR (1) FR2625196B1 (en)

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US5189220A (en) * 1988-07-29 1993-02-23 Rhone-Poulenc Chimie Process for preparing N-alkylanilines and N-allylanilines catalyzed by iodides
US5210305A (en) * 1988-07-29 1993-05-11 Rhone-Poulenc Chimie Process for preparing n-alkylanilines and n-allylanilines
US5276443A (en) * 1991-03-27 1994-01-04 Xircom, Inc. Parallel port multiplexor for PC parallel port
CN102040526A (en) * 2010-11-26 2011-05-04 西北师范大学 Preparation method of N,N-diallyl aniline

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US3642902A (en) * 1968-12-24 1972-02-15 Monsanto Co Allylamines from pi-allylpalladium complexes
US3914311A (en) * 1973-06-15 1975-10-21 Du Pont Preparation of aromatic secondary and tertiary amines using a nickel complex catalyst
US4096185A (en) * 1976-01-08 1978-06-20 E. I. Du Pont De Nemours And Company Preparation of p-aminobenzotrifluoride
EP0205391A1 (en) * 1985-05-22 1986-12-17 Rhone-Poulenc Chimie Process for the preparation of N-alkenyl-M-trifluoromethyl anilines

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FR2689503B1 (en) * 1992-04-03 1994-06-10 Solvay PROCESS FOR PURIFYING A HYDROFLUOROALKANE.

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US3642902A (en) * 1968-12-24 1972-02-15 Monsanto Co Allylamines from pi-allylpalladium complexes
US3914311A (en) * 1973-06-15 1975-10-21 Du Pont Preparation of aromatic secondary and tertiary amines using a nickel complex catalyst
US4096185A (en) * 1976-01-08 1978-06-20 E. I. Du Pont De Nemours And Company Preparation of p-aminobenzotrifluoride
EP0205391A1 (en) * 1985-05-22 1986-12-17 Rhone-Poulenc Chimie Process for the preparation of N-alkenyl-M-trifluoromethyl anilines

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CHEMICAL ABSTRACTS, vol. 83, no. 1, 7 juillet 1975, page 755, no. 9062t, Columbus, Ohio, US; N.M. MORLYAN et al.: "Copper(I) chloride, a catalyst for substitution of a halogen by amines in allylic halides", & ARM. KHIM. ZH. 1975, 28(1), 75-6 *

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DE3880997T2 (en) 1993-09-16
DE3880997D1 (en) 1993-06-17
JPH02739A (en) 1990-01-05
US4956496A (en) 1990-09-11
FR2625196A1 (en) 1989-06-30
ATE89259T1 (en) 1993-05-15
EP0322290A3 (en) 1990-05-02
FR2625196B1 (en) 1990-04-27
EP0322290B1 (en) 1993-05-12

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